CN102499418A - Electrical conduction oil ultra-high temperature instantaneous liquid sterilizer - Google Patents
Electrical conduction oil ultra-high temperature instantaneous liquid sterilizer Download PDFInfo
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- CN102499418A CN102499418A CN2011103571218A CN201110357121A CN102499418A CN 102499418 A CN102499418 A CN 102499418A CN 2011103571218 A CN2011103571218 A CN 2011103571218A CN 201110357121 A CN201110357121 A CN 201110357121A CN 102499418 A CN102499418 A CN 102499418A
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- tank body
- oil
- inner chamber
- sterilizer
- instantaneous liquid
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Abstract
The invention discloses an electrical conduction oil ultra-high temperature instantaneous liquid sterilizer, and solves the problems of large investment, large occupied land, high consumption, low security, unfavorable sterilization effect and the like of the conventional drink sterilization equipment. The sterilizer comprises a tank body provided with a vacuum interlayer, an electric heater mounted at the bottom of the tank body, and a spiral flow guide tube arranged in heat transfer oil in the inner chamber of the tank body; an oil inlet, an oil overflow opening and a discharge pipe are arranged at the top of the tank body respectively; an oil discharge opening and a feeding pipe are arranged at the bottom of the tank body respectively; the feeding pipe and the discharge pipe are connected and communicated with two ends of the spiral flow guide tube respectively; and slaked calcium powder with the mass percent of 0.1% and grass and stalk ash with the mass percent of 0.5% are added in the heat transfer oil. The sterilizer provided by the invention has the advantages of small investment, high security, remarkable effects of energy conservation and emission reduction, and good sterilization effect, can be applicable to sterilization of all liquid drinks, and has very remarkable social benefits.
Description
Technical field
The present invention relates to a kind of liquid sterilizing installation, specifically is the instantaneous liquid sterilizer of a kind of electric Oil Guide superhigh temperature.
Background technology
The sterilization of beverage is an of paramount importance step in the beverage production process process, and it is not only and guarantees the key of beverage in transportation and storage process, but also closely bound up with people's safe diet.The prior beverage sterilization mainly is to use the Boiler Steam sterilization; Secondly also have minute quantity radiation sterilization and ozone sterilization; Wherein, there are shortcomings such as equipment investment is big, floor space is many, energy resource consumption is high, effect is undesirable, security is low in the most widely used Boiler Steam sterilizing methods; And radiation sterilization and ozone sterilization can be mixed with a little residue in beverage, and health is had certain harm, generally seldom are used for food processing.Therefore according to energy-conserving and environment-protective, safe and efficient, thinking that low-cost high-efficiency is beneficial, design a kind of novel sterilizing installation, have great importance.
Summary of the invention
The objective of the invention is to invest problems such as big, that occupation of land is many, consume height, security is low, sterilization effect is undesirable, and provide a kind of electric Oil Guide superhigh temperature instantaneous liquid sterilizer in order to solve existing beverage sterilizing installation existence.Key of the present invention is existing coal burning boiler to be produced the steam UHTS change electricity consumption conduction oil generation UHTS into; Be added with special type in this conduction oil and add material; Make it can be heated to superhigh temperature (can reach 145-160 ℃), and non-volatile and evaporation, sterilization effect is better.
The present invention realizes through following technical scheme:
The instantaneous liquid sterilizer of a kind of electric Oil Guide superhigh temperature; Comprise the tank body of being with vacuum interlayer; The mozzle that spirals that is installed on the electric heater of tank base and places the tank inner chamber conduction oil, the top of tank body and bottom be respectively equipped with tank inner chamber in the mozzle that spirals be connected discharge nozzle and the feed pipe that communicates; The top of tank body also is provided with oil spill pipe and the oil-in that communicates with tank inner chamber, and tank base also is provided with the oil drain out that communicates with tank inner chamber, is respectively equipped with corresponding spill valve, inlet valve and draining valve on oil spill pipe, oil-in and the oil drain out; The heating tube of electric heater passes the bottom that the tank body base plate is placed on tank inner chamber; Conduction oil is injected in the tank inner chamber through the oil-in at tank body top, and is added with in this conduction oil and accounts for the careless straw ash that its mass percent is 1% ripe calcium powder and 0.5%.
During work; Conduction oil is injected in the tank inner chamber by the oil-in at tank body top; Place the mozzle that spirals of tank inner chamber with submergence; Start then and be located at the heater of tank base and the conduction oil in the tank inner chamber carried out heat, when conduction oil reaches the sterilisation temp of setting, drink liquid is entered in the mozzle that spirals from charging aperture through its heating tube; Drink liquid is through spiraling mozzle and by the conduction oil instantaneous sterilizing of superhigh temperature, and drink liquid is accomplished the sterilization back and derived from discharge nozzle.Wherein, the vacuum interlayer of tank body can play heat-insulation and heat-preservation to the conduction oil in the tank inner chamber; The tank body top is provided with the oil spilling mouth can discharge the unnecessary conduction oil that expands and seethe with excitement owing to heat in the tank body, to prevent the tank body blast; Be located at respective valves on oil spill pipe, oil-in, oil drain out and the discharging opening can be according to specific circumstances with require to open and close setting.
Further, described feed pipe is provided with force (forcing) pump, and thermometer, air gauge, air bleeding valve and bleeder valve are installed on the discharge nozzle successively.Thermometer of installing on the discharge nozzle and air gauge are in order to monitor the temperature and pressure of the drink liquid in the mozzle that spirals in real time, according to the variation of drink liquid temperature and pressure the force (forcing) pump on the feed pipe to be regulated accordingly; The air bleeding valve that is provided with on the discharge nozzle can carry out the exhaust step-down to sterilizer under special circumstances, and the pressure in the sterilizer is remained at below 2 MPas.
Described oil-in is opened on the sidewall of oil spill pipe and with oil spill pipe and is communicated with.
Also offer sight glass on the sidewall of described tank body.Can through sight glass intuitively, the real-time various situation of observing tank interior so that make corresponding adjustment.
Another big innovative point of the present invention also is the conduction oil of tank interior, and conduction oil is a kind of transmission medium of heat, has homogeneous heating; Advantages such as temperature adjustment control temperature is accurate; But existing conduction oil in order to prevent gasification volatilization even burning, all can not be heated to too high temperature when heating, so also just do not reach the purpose of sterilization; And the conduction oil among the present invention is owing to added 1.0% ripe calcium powder and 0.5% careless straw ash; Improved the boiling point of conduction oil greatly, made conduction oil can be heated to superhigh temperature (conduction oil among the present invention can be heated to 145-160 ℃), to meet the requirement of sterilization.
The invention has the beneficial effects as follows:
(1), energy-saving effect.Sterilizer of the present invention is than lacking with steam boiler sterilization energy resource consumption; The steam boiler ordinary production was rolled over 2.14 tons of standard coals with 3 tons of coals in one day, and one day power consumption of sterilizer of the present invention only needs about 90 degree; 0.007 ton of folding standard coal, energy-saving effect is quite obvious under the contrast.
(2), emission reduction effect.With the steam boiler sterilization, ordinary production was discharged 0.35 ton in waste residue with 3 tons of coals in one day at least, also had the form waste gas of sulfur dioxide discharging, and can reach zero-emission with sterilizer of the present invention, realized cleaner production.
(3), equipment operation and labour cost are low.Need use 3000 yuan in carbon with steam boiler, workman 3 people, wage needs 240 yuan every day, and it is 3240 yuan that other letter example is chargeed.And use sterilizer of the present invention, and the electricity charge are less than 80 yuan, and automaticity is high, only need a workman, and saving operating cost was 3080 yuan in one day.
(4), floor space is few.With the steam boiler sterilization, the boiler room takes up an area of about 10m
2, deposit charcoal field 300 m
2, sterilization tank 10 m
2, need 320 m altogether
2About the place.And sterilizer of the present invention only needs 2 m
2, save 318 m
2Place and building, reduce expenses 300,000 yuan.
(5), equipment is safe in utilization.Steam boiler is under HTHP, to sterilize; There is certain potential safety hazard; And sterilizer of the present invention has only high temperature and do not have a high pressure (pressure is lower than 2 MPas), and safety coefficient can be as the high explosive of steam pressure with steam boiler than with the steam boiler height.
(6), equipment and affiliated facility small investment.Same sterilization process adopts a cover steam boiler sterilizing installation need invest about 1,800,000 yuan, only needs about 300,000 yuan with sterilizer of the present invention, nearly 1,500,000 yuan of monetary savings.
Sterilizer of the present invention can be applicable to the sterilization process process in the various liquid beverages productions widely; As: liquid diary product beverage, fruit drink, juice beverage, vinegar beverage, vegetable protein beverage and soda etc.; Range of application is extremely wide, the social benefit highly significant.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Among the figure: 1-tank body, 2-electric heater, 3-spiral mozzle, 4-discharge nozzle, 5-feed pipe, 6-force (forcing) pump, 7-thermometer, 8-air gauge, 9-air bleeding valve, 10-bleeder valve, 11-vacuum interlayer, 12-oil spill pipe, 13-oil drain out, 14-oil-in, 15-spill valve, 16-inlet valve, 17-draining valve, 18-sight glass, 19-heating tube, 20-conduction oil.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is done further description:
As shown in Figure 1; The instantaneous liquid sterilizer of a kind of electric Oil Guide superhigh temperature; Comprise the tank body 1 of being with vacuum interlayer 11; The mozzle 3 that spirals that is installed on the electric heater 2 of tank body 1 bottom and places tank body 1 inner chamber conduction oil 20, the top of tank body 1 and bottom be respectively equipped with tank body 1 inner chamber in the mozzle 3 that spirals be connected the discharge nozzle 4 and feed pipe 5 that communicates; The top of tank body 1 also is provided with the oil spill pipe 12 and oil-in 14 that communicates with tank body 1 inner chamber; Tank body 1 bottom also is provided with the oil drain out 13 that communicates with tank body 1 inner chamber, is respectively equipped with corresponding spill valve 15, inlet valve 16 and draining valve 17 on oil spill pipe 12, oil-in 14 and the oil drain out 13; The heating tube 19 of electric heater 2 passes the bottom that tank body 1 base plate is placed on tank body 1 inner chamber; Conduction oil 20 is injected in tank body 1 inner chamber through the oil-in 14 at tank body 1 top, and is added with in this conduction oil 20 and accounts for the careless straw ash that its mass percent is 1% ripe calcium powder and 0.5%.
Further, described feed pipe 5 is provided with force (forcing) pump 6, and thermometer 7, air gauge 8, air bleeding valve 9 and bleeder valve 10 are installed on the discharge nozzle 4 successively.Described oil-in 14 is opened on the sidewall of oil spill pipe 12 and with oil spill pipe 12 and is communicated with.Also offer sight glass 18 on the sidewall of described tank body 1.
During practical implementation, the sterilization process process during sterilizer of the present invention is produced applicable to any liquid beverage, as: liquid diary product beverage, fruit drink, juice beverage, vinegar beverage, vegetable protein beverage and soda etc., range of application is extremely wide.
Claims (5)
1. instantaneous liquid sterilizer of electric Oil Guide superhigh temperature; It is characterized in that: the tank body (1) that comprises band vacuum interlayer (11); Be installed on the electric heater (2) of tank body (1) bottom and the mozzle that spirals (3) that places tank body (1) inner chamber conduction oil (20), the top of tank body (1) and bottom be respectively equipped with tank body (1) inner chamber in the mozzle that spirals (3) be connected discharge nozzle (4) and the feed pipe (5) that communicates; The top of tank body (1) also is provided with oil spill pipe (12) and the oil-in (14) that communicates with tank body (1) inner chamber; Tank body (1) bottom also is provided with the oil drain out (13) that communicates with tank body (1) inner chamber, is respectively equipped with corresponding spill valve (15), inlet valve (16) and draining valve (17) on oil spill pipe (12), oil-in (14) and the oil drain out (13); The heating tube (19) of electric heater (2) passes the bottom that tank body (1) base plate is placed on tank body (1) inner chamber; Conduction oil (20) is injected in tank body (1) inner chamber through the oil-in (14) at tank body (1) top, and is added with in this conduction oil (20) and accounts for the careless straw ash that its mass percent is 1% ripe calcium powder and 0.5%.
2. the instantaneous liquid sterilizer of electric Oil Guide superhigh temperature according to claim 1; It is characterized in that: feed pipe (5) is provided with force (forcing) pump (6), and thermometer (7), air gauge (8), air bleeding valve (9) and bleeder valve (10) are installed on the discharge nozzle (4) successively.
3. the instantaneous liquid sterilizer of electric Oil Guide superhigh temperature according to claim 1 and 2 is characterized in that: oil-in (14) is opened on the sidewall of oil spill pipe (12) and with oil spill pipe (12) and is communicated with.
4. the instantaneous liquid sterilizer of electric Oil Guide superhigh temperature according to claim 1 and 2 is characterized in that: also offer sight glass (18) on the sidewall of tank body (1).
5. the instantaneous liquid sterilizer of electric Oil Guide superhigh temperature according to claim 3 is characterized in that: also offer sight glass (18) on the sidewall of tank body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110357121.8A CN102499418B (en) | 2011-11-12 | 2011-11-12 | Electrical conduction oil ultra-high temperature instantaneous liquid sterilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110357121.8A CN102499418B (en) | 2011-11-12 | 2011-11-12 | Electrical conduction oil ultra-high temperature instantaneous liquid sterilizer |
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| Publication Number | Publication Date |
|---|---|
| CN102499418A true CN102499418A (en) | 2012-06-20 |
| CN102499418B CN102499418B (en) | 2014-04-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110357121.8A Expired - Fee Related CN102499418B (en) | 2011-11-12 | 2011-11-12 | Electrical conduction oil ultra-high temperature instantaneous liquid sterilizer |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101410765A (en) * | 2006-03-31 | 2009-04-15 | 卡西欧计算机株式会社 | Time correction control apparatus and method of time correction control |
| CN101480599A (en) * | 2008-12-30 | 2009-07-15 | 吕德斌 | Technique for heating and cooling material in reactor by heat carrier through jacket |
| CN201585388U (en) * | 2010-01-12 | 2010-09-22 | 河北艺能锅炉有限责任公司 | Sugar boiler for heating sugar through heat transfer oil via precision temperature control |
| CN201667963U (en) * | 2010-05-17 | 2010-12-15 | 王承辉 | Solar heating sterilization device |
| CN202311116U (en) * | 2011-11-12 | 2012-07-11 | 杜文 | Electric conduction oil superhigh temperature instant liquid sterilizer |
-
2011
- 2011-11-12 CN CN201110357121.8A patent/CN102499418B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101410765A (en) * | 2006-03-31 | 2009-04-15 | 卡西欧计算机株式会社 | Time correction control apparatus and method of time correction control |
| CN101480599A (en) * | 2008-12-30 | 2009-07-15 | 吕德斌 | Technique for heating and cooling material in reactor by heat carrier through jacket |
| CN201585388U (en) * | 2010-01-12 | 2010-09-22 | 河北艺能锅炉有限责任公司 | Sugar boiler for heating sugar through heat transfer oil via precision temperature control |
| CN201667963U (en) * | 2010-05-17 | 2010-12-15 | 王承辉 | Solar heating sterilization device |
| CN202311116U (en) * | 2011-11-12 | 2012-07-11 | 杜文 | Electric conduction oil superhigh temperature instant liquid sterilizer |
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| Publication number | Publication date |
|---|---|
| CN102499418B (en) | 2014-04-09 |
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Effective date of registration: 20160902 Address after: 045200, Shanxi Province, Yangquan County crown town crown village Patentee after: Ping Jin honey beverage company limited Address before: 045200, Shanxi Province, Yangquan County Crown Town, Yu Yu Ping Jin Jin honey beverage Co., Ltd. Patentee before: Du Wen |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140409 Termination date: 20191112 |
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| CF01 | Termination of patent right due to non-payment of annual fee |